Advanced Process Control Strategy for a Condensate Stabilization Unit: Energy, Exergy, Economic, and Environmental (4E) Study

被引:0
作者
Shafiei, Hamid [1 ]
Azin, Reza [2 ]
Osfouri, Shahriar [1 ]
Mohamadi-Baghmolaei, Mohamad [3 ]
机构
[1] Persian Gulf Univ, Fac Petr Gas & Petrochem Engn, Dept Chem Engn, Bushehr 7516913817, Iran
[2] Persian Gulf Univ, Fac Petr Gas & Petrochem Engn, Dept Petr Engn, Bushehr 7516913817, Iran
[3] Mem Univ, Dept Proc Engn, St John, NF A1C 5S7, Canada
关键词
NATURAL-GAS; CO2; EMISSION; HEAT-PUMP; OPTIMIZATION; DISTILLATION; EFFICIENCY; SYSTEM; PERFORMANCE; SIMULATION; INDUSTRY;
D O I
10.1021/acs.iecr.2c02964
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study assesses the energy, exergy, economic, and environmental performance of a gas stabilization unit by employing a new strategy to implement an advanced control system. The advanced process control (APC) strategy is established based on the response surface methodology to assess the real-time performance of the process. The RSMbased APC technique targets the energy, exergy, economic, and environmental (4E) performance of the process in unsteady-state operations. A detailed sensitivity analysis is also conducted to evaluate the relative significance of operating parameters on the objective functions, such as exergy efficiency, energy cost, and CO2 emission. The RSM-based APC strategy proposes an algorithm that can readily be implemented in the plant to increase the plant's energy performance. Implementing this intelligent control system leads to the production of standard products, while production cost, energy consumption, exergy efficiency, and environmental impacts are enhanced. The exergy and sensitivity results indicate that the stabilization tower has the highest potential for process enhancement, and reboiler temperature is the most influential factor among operating parameters. Also, the RSM-based APC improves the exergy efficiency of the plant by 19% and reduces the energy cost by 13%. At the optimal state, 457 kg/h CO2 emission is prevented.
引用
收藏
页码:3985 / 4001
页数:17
相关论文
共 63 条
[11]   Optimization of Operating Conditions for CO Hydrogenation to Hydrocarbon via Response Surface Method [J].
Delavari, Saeed ;
Nik, Hossein Mohammadi ;
Mohammadi, Nooshin ;
Samimi, Amir ;
Zolfegharifar, Sayyed Yaghoub ;
Antalovits, Ferenc ;
Niedzwiecki, Lukasz ;
Mesbah, Rashid .
CHEMICAL METHODOLOGIES, 2021, 5 (02) :178-189
[12]  
Di Pascoli S, 2001, ECOL ECON, V38, P179
[13]   The thermodynamic efficiency of energy complex enterprises processing raw gas condensate [J].
Dolotovsky, I. V. ;
Larin, E. A. ;
Dolotovskaya, N. V. .
OIL AND GAS ENGINEERING (OGE-2016), 2016, 152 :258-264
[14]   Exergy Analysis of Solid Fuel-Fired Heat and Power Plants: A Review [J].
Eboh, Francis Chinweuba ;
Ahlstrom, Peter ;
Richards, Tobias .
ENERGIES, 2017, 10 (02)
[15]  
El-Eishy M. M., 2019, PETROLEUM COAL, V61, P1378
[16]   Integration of vertical ground-coupled heat pump into a conventional natural gas pressure drop station: Energy, economic and CO2 emission assessment [J].
Farzaneh-Gord, Mahmood ;
Ghezelbash, Reza ;
Sadi, Meisam ;
Moghadam, Ali Jabari .
ENERGY, 2016, 112 :998-1014
[17]   Advanced process control system for a crude distillation unit. A case study [J].
Fayruzov, D. Kh. ;
Bel'kov, Yu. N. ;
Kneller, D. V. ;
Torgashov, A. Yu. .
AUTOMATION AND REMOTE CONTROL, 2017, 78 (02) :357-367
[18]  
Fitzsimons L., 2012, 9th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, (Malta)
[19]   Implementation of advanced control in the process industry without the use of MPC [J].
Forsman, Krister .
IFAC PAPERSONLINE, 2016, 49 (07) :514-519
[20]   Technology options for gas turbine power generation with reduced CO2 emission [J].
Griffin, Timothy ;
Buecker, Dominikus ;
Pfeffer, Allen .
JOURNAL OF ENGINEERING FOR GAS TURBINES AND POWER-TRANSACTIONS OF THE ASME, 2008, 130 (04)